Refrigeration



Sept." 18., 1945- A. RoswELL REFRIGERATIN `Filed April 2, 1943 2 Sheets-Sheet l -M/ 5 ATTORNEY x l .1 f f Sept. 18, 1945.

C. 'A. ROSWELL REFRIGERATION Filed April 2', 1943 l MTTORNEY Patented Sept. 18, 1945 l REFRIGERATION Charles Alfred Roswell, Newburgh, Ind., asslgnor to Servei, Inc., New York, N. Y., a corporation oi' Delaware Application April 2, 1943, Serial No. 481,519

l2 Claims.

This invention relates to refrigeration, and more particularly to refrigeration systems of the absorption type.

It is an object of the invention to provide an. 'improvement in refrigeration systems for transferring and removing non-condensible gases from one part, such as an absorber,l for example, to another part of the system. More specilicaily, it is an object to provide an improved auxiliary absorber for establishing positive dow of non-condensiblegases from an active part, such as the main absorber, for example, and to divert into such auxiliary absorber a part of the absorption liquid iiowing to the main absorber. The auxiliary absorber is relatively small compared to the part of the system from which the non-con densible gases are withdrawn in order that such gases may be localized in a small space.

By bringing the withdrawn non-condensible gases into intimatecontact with absorption liquid, refrigerant vapor accompanying the gases withdrawn from the main absorber is absorbed into solution, whereby the non-condensible 'gases are deprived of as much refrigerant vapor as possible. The absorption liquid, after being utilized to absorb refrigerant vapor from the non-l condensible gases, is employed to transfer the gases to a part of the system from which the gases may be exhausted to the atmosphere from time to time by a suitable vacuum pump.

The invention, together with the above and other objects and advantages thereof, will bebetter understood from the following description taken in connection with the accompanying drawings forming a part of this specication, and oi which:

Fig. l. more or less diagrammatically illustrates a refrigeration system embodying the invention; Figs. 2 and 3 are enlarged fragmentary views of parts shown in Fig. 1 to illustrate the invention more clearly; and

Figs. 4 and 5 are fragmentary views similar to Fig. 2 illustrating modiiications of the invention. Referring to Fig. 1, the invention is embodied in a two-pressure absorption refrigeration system like that described in United States LettersPatent No. 2,282,503 of A. R.. Thomas and P. P. Anderson, Jr., granted May 12, 1942. A sys-4 tem of this type operates at low pressures and includes a generator or vvapor expeller l0, a condenser Il, an evaporator l2 and an absorber Il which are interconnected in such a manner that the pressure dill'erential in the system is maintained by liquid columns. The disclosure in the aforementioned Thomas and Anderson patent may be considered as being incorporated in this application, and, ii desired, reference may be made thereto for a detailed description of the refrigeration system. I

In Fig. 1 the generator includes an outer shell it within which are disposed a plurality of vertical riser tubes i6 having the lower ends connected to receive liquid from a space i1 and the upper ends extending into and above the bottom of a vessel it. The space l@ within shell it forms a chamber to which steam is supplied through a conduit 2t from a suitable source of supply, so that full length heating of the tubes it is etlected. A vent 2i is provided at the upper end of shell ib, and-a conduit 22 is connected to the bottom part oi the shell for draining condensate from the space lil.

The system operates at a partial vacuum and contains a water solution of refrigerant in absorbent liquid such as, for example, a water solution of lithium chloride or lithium bromide. When steam is suppliedthrough conduit i@ to space Iii at atmospheric pressure, heat is supplied to tubes iii for expelling water vapor from solution. The absorption liquid is raised by-gas or vapor lift action, the expelled Water vapor forming a central core within an upwardly rising annulus of the liquid. In .vapor-liquid lifts of 'this character the expelled water vapor rises more rapidly than the liquid, and the liquid follows the vapor along the inside walls of the tubes it.

The water vapor discharged from the upper endsof the tubes or risers it separates from the `raised absorption liquid in the vessel it and' flows through a conduit 23 into condenser ii. The condensate formed in condenser il ows through a U-tube 24 into a chamber 26 and from the latter through a tube 26 into evaporator i2.

The evaporator i2 may include a plurality of horizontal banks of tubes 21 disposed one above the other and having heat transfer ns 28 se-- cured thereto to provide a relatively extendsive heat transfer surface. The liquid owing to evaporator l2 is divided in any suitable manner for ow through the uppermost bank of tubes 21. For examplathe dividing of liquid may be effected .by a liquid distributing trough 29 into which the liquid flows from the tube A26. The water iiows in successively' lower tubes through suitable end connections which are open' tov permit escape of vapor from thetubes. Any excess liquid re- Irigerant is discharged from the lowermost tubes 21. v The water supplied to tubes 21 evaporates therein to produce a refrigerating or cooling effect with consequent absorption of heat from the surroundings. as from a stream of air fiowing over the exterior surfaces of the tubes .il and ns 28. The vapor formed in tubes 2l passes out into end headers 30 which are connected at their lower ends to absorber Id. Any vapor formed in chamber 25 passes through a .conduit 3l into one of the headers 30 and mixes with vapor formed in the evaporator I2, so that disturbances in the evaporator due to vapor flashing of incoming liquid are avoided.`

In absorber i4 refrigerant vapor is absorbed into absorption liquid entering through a conduit 3i. The entering absorption liquid ows into a vessel 33 in which liquid is distributing laterally of a plurality of vertically disposed pipe banks 34 arranged alongside of each other. The liquid ows from vessel 33 through conduits 3b rinto a plurality of liquid holders and distributors 3B which extend lengthwise of and abovethe uppermost branches of the pipe banks 34. Absorp-I tion liquid is siphoned over the walls of the liquid holders 36 onto the uppermost pipe sections. Liquid drips from each horizontal pipe section onto the next lower pipe section, so that all of the pipe sections are wetted with a lm o liquid.

The water vapor formed in evaporator I2 passes through the headers 30 into the absorber I4 where it is absorbed by absorption liquid. Absorption liquid flows from absorber I4 through a conduit 31, a first group of passages In liquid heat exchanger 38, conduit 39, vessel 40, and conduit 4I into the bottom space I1 of generator I0. Water vapor is expelled' out of solution in generator I by heating, and liquid is raised by gas or vapor lift action in riser tubes I6, as explained above.

The absorption liquid in vessel I8. from'which refrigerant has been expelled from solution, ows through a conduit 42, another group of passages in liquid heat exchanger 38v and conduit 32 into the upper part of absorber I4. This circulation of absorption liquid is eii'ected by raising liquid i'n the vertical riser tubes I6 by vapor lift'actlon, so that liquid can ilow from generator I0 to absorber I4 and return from the latter back to the generator by force of gravity.

The upper part of vessel 40 is connected by conduit d3 to vessel I8, so that the pressure in vessel 4G is equalized with the pressure in the upper part oi generator I0 and condenser Il. The vessel 4|! is oi' suillcient volume to hold the liquid differential in the system and is of such cross-sectional area that the liquid level therein does not appreciably vary, so that a substantially constant reaction head is provided for lifting liquid in generator Ill.

The heat liberated with absorption of water vapor in absorber I4 is transferred to a cooling medium, such as water, which ilows upward through the vertically disposed pipe banks 34- The cooling medium enters the lower end of the pipe banks through a conduit 44 and leaves the upper end or' the pipe banks through a conduit 45. The conduit 45 may be connected'm condenser I i, so that the same cooling medium is utilized to eiect cooling of both the condenser II and absorber I4. From condenser II the cooling medium ilows through a conduit 46 to waste.

The system operates at low pressures with the generator I0 and condenser II operating at one pressure and evaporator I2 and absorber I4 operating at alower pressure, the pressure differ aseasei ential therebetween being maintained by liquid columns. Thus, the liquid column formed in tube 24 maintains the pressure diierential between condenser II and evaporator I2. The liquid column in conduit 3l maintains the pressure diiferential between the outlet of absorber I4 and generator I0, and the liquid column formed in conduit 32 and connected parts including conduit 4 2 maintains the pressure diierential between the inlet of the absorber and the upper part of the generator Ill. In operation, the liquid columns may form in conduits 3i, d2 and downleg of tube 24 to the levels m, y and s, for example. The conduits are of such size that restriction to gas flow is eiected without appreciably restricting flow of liquid.

During operation of the refrigeration system non-condensible gases may collect in the ysystem, and in condenser il such gases now toward the dead-end or bottom part of the condenser. To transfer and remove non-condensible gases from condenser II to the lower pressure side of the system, a liquid trap 41 is provided in U-tube 26. `Liquid formed in condenser II flows into trap 41, and, when the trap is completely iilled with liquid to the level c, the liquid is siphoned from the trap into the downleg of U-tube 2d. The gas in the downleg of U-tube 24. in the region between the trap 41 and the liquid level at z, is trapped by the liquid siphoned from the liquid trap 41. Immediately after liquid has siphoned from the liquid trap 41, gas passes from the bottom part of condenser II through the trap 41 into the downleg of U-tube 24. When liquid passing from condenser II again reaches the level c in the trap 41, liquid is again siphoned into the downleg of the tube 24. In this manner gas passing from condenser II into the downleg oi the tube 24, before the liquid seal is formed in trap 41, is segregated by the liquid subsequently siphoned into the downleg of the tube.

'I'he gas segregated between the successive bodies of liquid siphoned from trap 41 is comf pressed by the siphoned liquid and passes through the U-tube 24 from condenser II to evaporator l2. In this way non-condensible gases collecting in the upper part of generator I0 and condenser II are transferred from these parts of the system to the evaporator l2 andk absorber I4.

In accordance with this invention an improved auxiliary absorber :il is providedgfor removing refrigerant vapor from non-condensible gases withdrawn from the main absorber I 4, so that positive now of-non-condensible gases from absorber Ill is efected and at the same time such gases will be deprived of as much refrigerant vapor as possible. The auxiliary absorber l is considerably smaller than the main absorber I in order to localize the non-condensible gases, and includes an outer shell 48 into the upper part of which the gases pass through a conduit 139 from the bottom part of absorber i4.

Within the shell 48 is disposed a tube 5D having top and bottom closure members 5I and 52, respectively, as shown most clearly in Fig. 2. Concentrically arranged within tube 50 and spaced therefrom is a cylindrical screen 53 having the ends thereof fitting over shoulders formed on the closure members 5I and 52. A liquid. deflecting plate 54, which is fixed to an extension of the top closure member 5I, is positioned above a small opening or restriction 55 formed in the top closure member. The top closure member 5I serves as an inlet for absorption liquid which is introduced into the auxiliary absorber through lase-.acci

a conduit 56. As shown in Fis. 1, the upper end of conduit 56 is connected to the upper part of conduit 32 through which absorption liquid flows to the upper part of absorber I4. V

A cooling coil 51 is disposed about and in thermal contact with tube 50. The lower end of coil 51 is connected by a conduit 58 to conduit 44, and the upper end thereof is connected by aconduit 59 to conduit 45. With this arrangement a part of the cooling water ilowing to the` main absorber I4 through conduit 44 is diverted into coil 51 of the auxiliary absorber 41. The cooling water passing from the upper end of coil 5.1 joins cooling water in conduit 45 passing from the upper part of the main absorber I4.

To the bottom part of shell 48 is connected the upper curved;or lrounded portion 60 of a vertically extending tube GI. The lower end of tube I is connected at 62 to the bottom part of a` vertical conduit 63. The bottom part of conduit l t3 in turn is connected by a short conduit 64 to the conduit '81 through which absorption liquid iiows from the outlet of absorber Ill. It will be observed from the foregoing description that the conduit 5d, auxiliary absorber t1, vertical tube ti, lower end of the tube tt and conduit tl constitute a. Toy-pass between the conduits 32 and 31 coizistitutiner separate paths of iljow for absorption solution between the absorber It and gener? ator it. It also lwill be observed that the by-pass will receive absorption liquid from the conduit 32 at the low pressure prevailing in the absorber 'It and will deliver absorption liquid to the conduit t1 at the high pressure prevailing inthe generator I ii.

To the upper end of conduit 53 is connected a vessel odas shown in Fig. 1. The vertical conduit t3 and vessel 5b constitute the part to which non-condensi-ble gases aretransferred from absomber It, as which will be described presently. A vacuum pump Bt may be connected by a conduit 61 to the vessel 55 for withdrawing non-condensiblegases from the System. A suitable valve the gases withdrawn from absorber I4 and also remove as much refrigerant vapor as possible from the withdrawnl gases. The absorption liquid diverted from conduit 52 into conduit |55 ows by gravity tothe auxiliary absorber into the cylindrical screen` 53 therein. Liquid passes through screen 53 into the annular space between the screen and the tube 50, and is discharged through the oriiice or opening 55. The screen t8 is provided in conduit 51 to maintain the system at a low pressure.

During operation of the refrigeration system, non-condensible gases may collect in generator i0 and condenser Il forming the high pressure side of the system. Suchgases are swept by the refrigerant vapor flowing from generator yI0 into condenser il and are carried to the far end of the condenser at the region to which the tube' 24 is connected. It is for this reason that trap 41 is provided in the downleg of tube 24 to transfer non-.condensible gases from condenser II to evaporator I2,\-as explained above.

The non-condensible gases collecting in the .evaporator I2 and absorber I4, which form the low pressure side of the system, are carried to the bottom part oi. the `absorber. This downward movement is imparted to the non-condenstble gases by the high velocity refrigerant vapor no wing into the absorber. In a refrigeration system like that described and having an ice meltingl 1 ycapacity of ve tons, for examplathe average velocity of the refrigerant vapor escaping from the evaporator I2 to absorber I4 under ordinary operating conditions is about 130 feet per secand. Thus, the high velocity refrigerant vapor forces the non-condensible gases to the bottom lof the absorber midway between the headers 3U.

In removing and transferring non-condensible gases from absorber I4 to vertical conduit 5; and vessel 55 associated therewith, the auxiliary abporber" is utilized to establish positive ilow of -53 removes foreign matter from the absorption restricts flow of liquid therethrough to limit the rate at which liquid is diverted from conduit 32 into the. auxiliary absorber 41.

Under the small pressure head of liquid in conduit 56, absorption liquid spouts upwardly from orifice 55 and strikes the dectlecting plate 54. This causes the liquid to flow downwarly over the top closure member 5I onto the surface oi' 'the uppermost turn of coil 51. Both the edges of the deecting plate 154 and top closure member 5I are more or less in vertical alignment with the uppermost turn of coil 51, sothat liquid will readilyn drip from the plate 5t and closure member 5i onto the coil 51. The liquid news over the exterior surface of coil 51 and forms a liquid film thereon to provide a. relatively extensive iiduid surface.

The non-'condensible gases passing from the bottom of main absorber I4 through conduit M into the auxiliary absorber 41 come in intimate contact with the nlm of absorption liquid 'on the coil t1. Refrigerant vapor accompanying the noncondensible gases is absorbed into absorption liquid, and the heat liberated with such absorption or refrigerant vapor is transferred to the cooling '-water flowing through coil 51. Y

The absorption liquid in the bottom part o the auxiliary absorberl enters the upper roundof the tube. When liquid'siphons from the bent portion su of tube sl, the liquid level fans in the bottom part of the auxiliary absorber 41 sumciently so that non-condensible gases can pass into the bent portion B5. When the liquid level inthe bottom part of the absorber 41 again rises' sufdciently. the upper bent portion 5o is closed oir and a small quantity of liquid is again siphoned into the tube 6I. Infthis way small quantitles of non-condensible gases are withdrawn from the bottom part of the auxiliary absorber 41 and trapped between successive bodies or slugs of liquid formed at the upper bent portion 5l of the tube 8l. The tube -SI mayl be referred to as a fall tube pump and is of such size that ilow of liquid is not appreciably restricted, and yet the internal diameter is such thatvgas and liquid cannot pass eachother while ilowing downwardly .throughy the tube. When a solution of lithium bromide of about 55%'ooncentration by weight is employed in a system of the type described, a falltube pump having an internal diameter of about 0.180" has operated in a satisfactory manner to mi), small quantities of gas between slugs of liq- The gas trapped between slugs of liquid in' tube 6I is comprsed as the liquid and gas pas:

downwardly in the tube. From the lower end of tube iii the trapped gas is discharged into the bottom of conduit 63 which is of considerably greater' size than tube 5i, so that the gas bubbles will freely pass upwardly through liquid therein, as diagrammatically shown in 3;

als the quantity of non-oondensi' transerred to conduit and vessel En in liquid level in conduit 53 falls duc to the gases displacing liquid therefrom. The liquid displaced from conduit 53 passes through conduit fait .into conduit 3l. rl'he vacuum pump may be used as desired to exhaust ncn-condensible gases from conduit 63 and vessel b5 into the atmosphere.

By transferring the non-condensible gases in the system into the conduit 53 and vessel b5, several advantages result. First, the non-condensible gases cannot accumulate in other parts of the system such as the condenser li and absorber it, for example, and occupy and blanket olr` space in these parts that otherwise would be occupied by refrigerant vapor. Further, objectionable increase of pressure in the condenser and absorber 'that would result with accumulation of noncondensible gases in these parts is avoided by constantly removing and transferring the gases to a part of the system like that formed by conduit 63 and vessel t5.

By transferring the non-condensible gases in the system to vertical conduit 63 and vessel 65, such gases are removed from all parts of the systern actively participating in the production of refrigeration and collected in a single place which might be referred to as an inactive part. 'The non-condensible gases accumulating in the inactive part formed by conduit t3 and vessel S5 can reach a, pressure considerably greater than that existing in the active parts in both th'e high and lower pressure sides of the system. For example, in the system like that referred to above and having an ice melting capacity of about five tons, and in which a solution of lithium bromide ofk about 55% 'concentration by weight is employed, the pressures in the high and lower pressure sides of the system are about 55 and 9 mm.

lig, respectively. Under these conditions the pressure in vessel 5E above the liquid level e therein is 56 mm. Hg, the pressure existing in the high pressure side of the system.

The maximum pressure tha canprevail in vessel and conduit t3 is reached when the liquid falls to the minimum level s in conduit 53. This maximum pressure in conduit 53 in the system referred to above is about 100 mm. Hg, and this pressure is balanced on the high pressure side of the system by the pressure above the liquid level e in vessel il@ and the liquid column extending downwardly from vessel lll through conduit t and one group of passages in liquid heat exchanger 33 to which the lower end of vertical conduit 63 is connected. Thus, while the pressure in the high' pressure side of the system is about 56 mm. Hg, the non-condensible gases can be trapped inconduit 53 and vessel t5 to a maximum pressure of about 3.00 mm. Hg, and at the same time the trapped gases do not adversely aect the normal operation of nor impairthe eiciency of the refrigeration system. The auxiliary absorber dla illustrated in 4 diiers from that shown in Fig. 2 and described above in that the screen 53a and orice or metering device 55 are located outside of shell lila in a separate housing 70.k In Fig. 4 cooling` water diverted from conduit 44 through' conduit 58 is introduced into the lower end of a hollow cylinder'or tube 50a extending upwardly within shell @8a. The'cooling water passes from the upper curved end of tube 5Go into the upper end of 'a coil 51o disposed about and in thermal contact with the tube. The lower entf. of coil 57a .is connected by conduitl it i, sonduit #l5 in the saine manner as in the first embodiment described above and shown in Fig. i.

In the embodiment illustrated in Eig. 4 diverted absorption liquid discharged from the lower end of conduit 5S strikes the upper closed end of tube 5ta at which region the non-condensible gases enter through conduit from the main absorber I d. The absorption liquid ilows along the coil Ela and forms a liquid nlm therein to provide a relatively extensive liquid surface with which the gases come in contact. Refrlgerant vapor aacompanying the non-condensible gases is absorbed into the absorption liquid and in this way is removed from the gases. The heat liberated with absorption of refrigerant vapor into solution is transferred to the cooling water ilowing through coil 57a. From auxiliary absorber lla the non-condensible gases are transferred through the fall tube pump 5l to the conduit E3 and vessel 65 in the same manner as in the iirst embodiment described above.

The embodiment shown in Fig. 5 diers. from that illustrated in Fig. el in that a solid helical member lb is disposed about and in thermal contactl with tube 5th, and the cooling water circulates entirely within the tube. In Fig. 5 the cooling water diverted from conduit lil through conduit 58 enters a conduit ll which is more or less a continuation of conduit 5B and extends upwardly within tube ilb. The cooling water is discharged from the upper end of conduit 'll adjacent the closed upper end of tube 5G11 and flows down over the exterior surface or conduit 'll and through the tube 58h. The cooling water passes from the lower end of tube 5th into conduit 59.

In Fig. 5 the non-condensible gases enter the auxiliary absorber lib through conduit til and come in contact with absorption liquid entering through conduit 5S. The absorption liquid strikes the upper closed end of tube b and ilows downwardly along the helical member 'b to provide al relatively extensive liquid surface. Reirigerant vapor accompanying the non-condensible gases is absorbed into absorption liquid, and the resulting heat of absorption is transferred to cooling water flowing downwardly within tube 59h.

By providing an auxiliary absorber like the absorbers l'l, Lila and ll'lb described above, refrigerant vapor is effectively removed from the noncondensible gases, so that substantially no refrigerant vapor accompanies the non-condensible gases trapped in the upper end of fall tube pump 6l. With substantially no refrigerant vapor entering the fall tube pump El, practically no absorption of refrigerant into absorbent takes place in the fall tube pump to produce objectionable noises and undesirable slowing down of the rate at which gas is transferred from absorber lil to vertical conduit 63. Hence, the auxiliary absorbers serve to effect withdrawal ofv non-condensible gases at a maximum rate into the fall tube pump 6I. In addition, since the absorption liquid diverted into the auxiliary absorbers fll, fila and ill? is weak in refrigerant while the absorbent in the bottom of the main absorber lll is rich in refrigerant, the vapor pressure of refrigerant in the auxiliary absorbers is less than that at the ing a casing providing a chamber, a hollow cylindrical member within said chamber having top and bottom closure plates, a helical coil tting snugly about said cylindrical member in direct contact therewith and extending lengthwise thereof, an annularscreen within and spaced from said cylindrical member, means for introducing absorption liquid within said annular screen, said top closure plate having an opening through which liquid is discharged upwardly from within said cylindrical member, means including a plate positioned above said cylindrical member ior delecting liquid discharged through the opening onto said coil, said cylindrical member and coil forming a downward path of new for absorption liquid, and means for 'Flowing a cooling medium through said coil.

A refrigeration system operable below atmospheric pressure and comprising a plurality of parts including a rst rabsorber interconnected Y for circulation of absorption liquid and refrigerant, and inea-ns including an auxiliary absorber for withdrawing non-condensible gases from said first absorber, said auxiliary absorber comprising a casing providing a chamber within which is disposed an upright hollow cylinder, a helical coil tting snugly about said cylinder in direct contact therewith and extending lengthwise thereof, means to iiow a cooling medium through said helical coil, and means to flow absorption liquid onto an upper part of said coil, said cylinder and coil forming a path of dow for absorption liquid in which liquid descends 'from one part of said coil onto a part of said cylinder and from the latter onto the next successively lower turn of the coil, so that'iresh liquid surfaces are constantly being provided with which non-condensible gases from said iirst absorber come incontact for removing rerigerant vapor accompanying such gases.

a helical element snugly fitting about and extending lengthwise of said member, means for 5. A refrigeration system operable below at mospheric pressure and comprising a plurality of parts including a rst absorber interconnected for circulation of absorption liquid and refrigerant, and means including an auxiliary absorber for withdrawing non-condensible gases from said rst absorber, said auxiliary absorber' comprising a casing providing a chamber within which is located a vertically disposed hollow cylindrical member, a. helical coil disposed about and extending lengthwise of said cylindrical member, means for introducing a cooling :medium to the lower part of said cylindrical member, the upper end of said coil being connected to the upper part of said cylindrical member so that cooling medium ows downwardlythrough said coil, and means to now absorption liquid onto an upper part of said coil, said colland cylindrical member forming a path of flow for absorption liquid in which liquid descends from one turn of said coil onto a part of said cylindrical member and from the latter onto the next successively lower turn of said coil, so that fresh liquid surfaces are constantly being provided with which non-condensible gases from said iirst absorber come in contact for vremoving refrigerant vapor accompanying such gases.

6. A refrigeration system operable below atmospheric pressure and comprising a plurality of parte including a first absorber interconnected for circulation of absorption liquid and refrigerant, and means including an auxiliary absorber for withdrawing non-condensible gases from said rst absorber, said auxiliary absorber comprising a casing providing a chamber within which is disposed an upright hollow cylindrical member,

circulating cooling medium within. said cylindrical member, and means to flow absorp" n liquid onto an upper part of saidelement, helical element and cylindrical member form i of flow for absorption liquid in which scends from one turn of said elemen" of said cylindrical member and from onto the next successively lower turn o ment.

'LA refrigeration system operable below otmospheric pressure and comprising a plurex for circulation of absorption liquid i ant, and means including an n for withdrawing non-condensible gases from sa* 1V first absorber, said auxiliary absor' er comprising a casing providing a chamber within located a vertically disposed hollow cf'indrical member, a tube extenA g upwardly member and terminating .n of, means for supplying cooling metube, said `cylindrical. member having outl t for the cooling medium in the lower part thereof, a helical element snugly fitting about and extending lengthwise of said member, and to flow absorption liquid onto an upper part oi said element, said element and cylindrical member forming a path of flow for absorption liquid in which liquid descends from one turn of said ele ment onto a part of said cylindrical member and from the latter onto the next successively lower turn of said element. l

8. A refrigeration system operable below atmospheric pressure and having a plurality of active parts, said active parts bein-g interconnected for circulation of absorption liquid and refrigerant, `and means including an absorber for withdrawing non-condensible gas from one of said active parts, said albsorber having a vertically dis posed cylindrical wall, a vertically extending pipe coil directly .contacting a surface of said wall, said absorber being connected to receive non-condensi- Ible gasfrom said one active part, and means for iiowing absorption liquid onto an upper of said coil, said cylindrical wall and coil form ing a path of flow for absorption liquid in which liquid descends from one turn of said coil onto a part of said surface and from the latter onto the next successively lower turn of said coil.

9. A refrigeration system operable below atmospheric pressure and comprising a plurality of active parts including a rst absorber interconnected for circulation of absorption liquid and refrigerant, a vertically extending tube embodied in the system andithrough which absorption liquid ows, the upper endfof said tube being in communication With said first absorber, and means including said tub'e for withdrawing non-condensi ble gas from said first absorber, said means inu cluding an auxiliary absorber for 'locaiiring the non-condensible gas flowing from said first ab sorber and for removing therefrom accompanying refrigerant vapor, said auxiliary absorber in cluding a vertically disposed cylindrical wall a pipe coil directly contacting a surface of such wall, and means Tor flowing absorption liquid onto an upper part of said coil, the refrigerant vapor accompanying the non-condensible gas from said ilrst absorber being absorbed into absorption liqd uid in said auxiliary absorber whereby gas substantially free of refrigerant is entrained by alisorption liquid at the upper end o said tube.

10. In an absorption refrigeration system coniprising a plurality of elements including van absorber interconnected to provide a closed circuit /auxiliary absorber utilizing the aibsorption liquid to absorb refrigerant vapor and create a relative partial vacuum whereby to cause flow of the gases from the absorber to the auxiliary absorber, means for supplying a cooling medium to the auxiliary absorber to remove the heat of absorption, and means for withdrawing non-condensible gases from the auxiliary absorber.

11. In an absorption refrigeration system comprising a generator and condenser operable at one pressure and an evaporator and albsorber operable at a lower pressure, means interconnecting the elements to provide a closed circuit for the circulation of a refrigerant and absorption liquid and maintain the pressure differential, an auxiliary absorber connected to the low pressure side of the system to receive non-condensible gases therefrom, means for supplying absorption liquid weak in refrigerant to the lauxiliary absorber, said auxiliary absorber utilizing the absorption liquid to absorb refrigerant vapor to cause a. ow of the gases thereto, means for supplying a cooling heat of absorption. and means for withdrawing 'non-condensible gases from the' auxiliary absorption liquid weak in refrigerant and absorp tion liquid strong in refrigerant, a by-pass connected between the separate paths of iiow to cause absorption liquid weak in refrigerant to ow therethrough, an auxmmabsorber in the by` pass and connected -to the low. pressure side of the system to receive non-conde ilble gases therefrom, said auxiliary aibsorbeil'lsxg sorptlon liquid iiowing therevthro i1 for absorbing refrigerant vapor to cause a flow of gases thereto, means for supplying a. cooling medium to the auxiliary absorber -to remove the heat of absorption, and a fall tub'e pump in the 'oy-pass for withdrawing thenonhcondensible gases from the auxiliary absorber.

- medium to the auxiliary absorber toremove the tilizing the ab- 4 

